EP0108249A1 - Procédé de séchage de gypse humide, particulièrement de gypse provenant d'une installation de désulfurisation par voie humide de gaz brûlés et dispositif pour mettre en oeuvre ce procédé - Google Patents

Procédé de séchage de gypse humide, particulièrement de gypse provenant d'une installation de désulfurisation par voie humide de gaz brûlés et dispositif pour mettre en oeuvre ce procédé Download PDF

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Publication number
EP0108249A1
EP0108249A1 EP83109888A EP83109888A EP0108249A1 EP 0108249 A1 EP0108249 A1 EP 0108249A1 EP 83109888 A EP83109888 A EP 83109888A EP 83109888 A EP83109888 A EP 83109888A EP 0108249 A1 EP0108249 A1 EP 0108249A1
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EP
European Patent Office
Prior art keywords
gypsum
air
drying air
furnace
drying
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP83109888A
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German (de)
English (en)
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EP0108249B1 (fr
Inventor
Klaus Dr. Ing. Hannes
Helmut Ing. Grad. Weiler
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Steag GmbH
Knauf Engineering GmbH
Original Assignee
Steag GmbH
Knauf Engineering GmbH
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Publication date
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Application filed by Steag GmbH, Knauf Engineering GmbH filed Critical Steag GmbH
Priority to AT83109888T priority Critical patent/ATE18541T1/de
Publication of EP0108249A1 publication Critical patent/EP0108249A1/fr
Application granted granted Critical
Publication of EP0108249B1 publication Critical patent/EP0108249B1/fr
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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00—Compounds of calcium, strontium, or barium
    • C01F11/46—Sulfates
    • C01F11/464—Sulfates of Ca from gases containing sulfur oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/48—Sulfur compounds
    • B01D53/50—Sulfur oxides
    • B01D53/501—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B11/00—Calcium sulfate cements
    • C04B11/02—Methods and apparatus for dehydrating gypsum
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Definitions

  • the invention relates to a method for drying moist gypsum, in particular gypsum from a wet chemical flue gas desulfurization system, by means of flue gases from combustion systems, in particular from coal-fired power plants, in which between the air which is at least partly supplied to the furnace as combustion air and that from the furnace escaping smoke gases heat is exchanged.
  • the boiler has a heat exchanger, e.g. B. a rotary heat exchanger, downstream, to heat the air required for the combustion and drying of the coal in the boiler upstream coal mills by means of the hot flue gases emerging from the boiler.
  • a heat exchanger e.g. B. a rotary heat exchanger
  • the gypsum emerging from such a flue gas desulphurization plant often has to be subjected to drying in order to enable its further processing and / or transport.
  • a dust filter e.g. B. in the form of an electrostatic filter.
  • part of the dedusted hot flue gas stream is branched off in front of the flue gas desulfurization system and fed to the dryer.
  • the drying air can be separated from the plaster and released into the atmosphere; in most cases, however, a separate fine dust filter may be required here.
  • the drying air is separated from the gypsum after at least part of its heat has been released and is fed to the furnace. This ensures that the existing residual heat is used and that the dust filter downstream of the combustion system can also be used for the dedusting of dry air.
  • This dedusting device can, for. B. the combustion system downstream dust filter itself or a dry or wet chemical flue gas desulfurization system.
  • the latter possibility offers z. B. in cases where the flue gas desulfurization z. B. can be used in the cement industry.
  • the drying air need not have been finely dedusted, but rather roughly dedusted drying air can be fed into the path of the flue gases.
  • the method can also be used to dry other chemical gypsum, the advantages of the method according to the invention become particularly clear when the flue gases from the combustion system are desulfurized in a wet chemical flue gas desulfurization system and the wet gypsum removed from the flue gas desulfurization system is dried with the drying air.
  • the invention is also directed to a device for carrying out the method and is based on a device with a combustion system, a dryer which can be loaded with moist gypsum and can be operated with warm gas, and a heat exchanger, in particular rotary air preheater, which is connected upstream of the combustion air side and downstream of the flue gas side.
  • the outlet of the heat exchanger for the heated air is connected to the hot gas inlet of the dryer.
  • a separator in which the dried gypsum is separated from the drying air, is preferably connected downstream of the dryer.
  • the drying air outlet of the separator is connected to the combustion system; the connection can preferably be made directly with the furnace or between the furnace and dust filter.
  • Coal K is fed to a coal mill 1 and from there via a conveyor line 2 into the furnace of a boiler 3 introduced.
  • the flue gases R leave the boiler via a channel 4, which leads them to a rotary air preheater 5.
  • the cooled flue gas is fed to an electrostatic filter 7 via a channel 6.
  • the dedusted flue gas is fed via a channel 7a to a wet chemical flue gas desulfurization system 8. Examples of such wet chemical flue gas desulfurization plants can be found on pages 724 and 725 of the "Yearbook of Steam Generation Technology" (1980/81), Vulkan-Verlag, Essen.
  • the flue gas desulfurization system 8 is a detergent, z. B. a lime suspension or a lime-HCl solution.
  • the gypsum produced in the flue gas desulfurization system 8 is introduced via a line 10 into a dryer 11, in which the moist gypsum can be dried by means of warm air GL supplied via line 12.
  • a dryer is suitable for.
  • B. the device known from DE-PS 21 55 240;
  • Another preferred option for the dryer is the known flight layer dryer.
  • the combustion and drying air required for the operation of the combustion system consisting of one or more coal mills 1 and a boiler 3 connected downstream of this is led to the rotary air preheater 5 via a pressure blower 13 and a duct 14 and the heated air is supplied via a duct 15 and branch lines 15a and 15b are fed to the boiler 3 as combustion air VL and the mill 1 as coal drying air KL.
  • the duct 15 continuing from the Luvo 5 is connected to the duct 12.
  • a flap 16 and a heat exchanger 17 to which steam D can be applied are arranged in the channel 12.
  • the heat exchanger 17 can be steam of the boiler 3 are applied.
  • the corresponding steam lines have been omitted from the figure.
  • the channel 14 is connected to the channel 12, the connection point being between the flap 16 and the heat exchanger 17.
  • a flap 19 is arranged in the connecting line 18 itself.
  • the dried gypsum and the drying air GL are withdrawn from the dryer 11 via a channel 20 and fed to a separator 21, which is preferably designed as a cyclone.
  • the exhaust air from the separator 21 is fed into the branch line 15a via a duct 22.
  • valves or flaps can be arranged to adjust the flow cross sections. For the sake of simplicity, these are not shown.
  • the end product i.e. the dried gypsum
  • the desulfurized flue gas is fed to a chimney 26 by means of a duct 24 in which a suction fan 25 is arranged.
  • the ratios can be designed so that particular during operation of the combustion plant with a coal moisture content of a portion of the heated air in the duct 15 via K anal can be peeled 12 and the drying can be used in the dryer. 11 Should the moisture content of the coal decrease, the proportion of drying air KL can be reduced and the drying air GL can be increased. With particularly moist coal, it may be necessary for the heat exchanger 17 to be put into operation for a short time must, in order to increase the temperature of the air GL supplied to the dryer to drying temperature via channel 12.
  • a bypass can be assigned to this heat exchanger in order to guide air GL around it when the heat exchanger is not in operation.
  • This can serve to heat the air branched off from the duct 15 and / or the air brought in via duct 18. With the help of valves 16 and 19, the amounts of air can be adjusted. If the flue gas heat for heating up the drying air is not available, the drying air GL for the gypsum is heated exclusively by means of steam D.
  • the amount of water to be expelled from the coal during the grinding and the amount of water to be expelled from the gypsum when drying is behaving approximately like 10: 1, so that the air quantity GL in duct 12 and the air quantity KL in duct 15b behave accordingly.
  • the heated air quantity GL required for drying the gypsum can in most cases be branched off from the duct 15 without difficulty for the operation of the power plant or reserves of the blower 14 and the Luvo's 5 can be used.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Ceramic Engineering (AREA)
  • Structural Engineering (AREA)
  • Environmental & Geological Engineering (AREA)
  • Geology (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Inorganic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Drying Of Solid Materials (AREA)
  • Treating Waste Gases (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
EP83109888A 1982-10-09 1983-10-04 Procédé de séchage de gypse humide, particulièrement de gypse provenant d'une installation de désulfurisation par voie humide de gaz brûlés et dispositif pour mettre en oeuvre ce procédé Expired EP0108249B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT83109888T ATE18541T1 (de) 1982-10-09 1983-10-04 Verfahren zum trocknen von feuchtem gips, insbesondere gips aus einer nasschemischen rauchgasentschwefelungsanlage und vorrichtung zur durchfuehrung des verfahrens.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3237474A DE3237474C2 (de) 1982-10-09 1982-10-09 Verfahren zum Trocknen von feuchtem Gips, insbesondere von Gips aus einer naßchemischen Rauchgasentschwefelungsanlage
DE3237474 1982-10-09

Publications (2)

Publication Number Publication Date
EP0108249A1 true EP0108249A1 (fr) 1984-05-16
EP0108249B1 EP0108249B1 (fr) 1986-03-12

Family

ID=6175331

Family Applications (1)

Application Number Title Priority Date Filing Date
EP83109888A Expired EP0108249B1 (fr) 1982-10-09 1983-10-04 Procédé de séchage de gypse humide, particulièrement de gypse provenant d'une installation de désulfurisation par voie humide de gaz brûlés et dispositif pour mettre en oeuvre ce procédé

Country Status (3)

Country Link
EP (1) EP0108249B1 (fr)
AT (1) ATE18541T1 (fr)
DE (2) DE3237474C2 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1987005530A1 (fr) * 1986-03-19 1987-09-24 Insinööritoimisto Lisop Oy Procede de purification de gaz de fumee
DE3626912A1 (de) * 1986-08-08 1988-02-11 Knauf Westdeutsche Gips Komprimate aus getrocknetem rauchgasgips und verfahren zur herstellung derselben
EP0266571A1 (fr) * 1986-10-08 1988-05-11 Noell-KRC Umwelttechnik GmbH Procédé de conversion des résidus des installations de désulfurisation par voie humide de gaz brulée

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2727544A1 (de) * 1977-06-18 1979-01-04 Heinz Hoelter Verfahren zur trocknung und umwandlung von chemiegips-dihydrat bis zum gips-halbhydrat durch nutzung von abgaswaerme hinter rauchgasentschwefelungsanlagen bei gleichzeitiger rauchgaskonditionierung fuer die nasse rauchgaswaesche
DE2931599A1 (de) * 1978-08-08 1980-02-21 Coal Industry Patents Ltd Verfahren und vorrichtung zum behandeln eines in getrennter form vorliegenden materials
DE3119422A1 (de) * 1980-05-24 1982-11-25 Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck "hybridverfahren mit dammbaustoff-endprodukt unter nutzung der abfallwaerme vor der rauchgasentschwefelung"

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2727544A1 (de) * 1977-06-18 1979-01-04 Heinz Hoelter Verfahren zur trocknung und umwandlung von chemiegips-dihydrat bis zum gips-halbhydrat durch nutzung von abgaswaerme hinter rauchgasentschwefelungsanlagen bei gleichzeitiger rauchgaskonditionierung fuer die nasse rauchgaswaesche
DE2931599A1 (de) * 1978-08-08 1980-02-21 Coal Industry Patents Ltd Verfahren und vorrichtung zum behandeln eines in getrennter form vorliegenden materials
DE3119422A1 (de) * 1980-05-24 1982-11-25 Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck "hybridverfahren mit dammbaustoff-endprodukt unter nutzung der abfallwaerme vor der rauchgasentschwefelung"

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Patent Abstracts of Japan Band 2, Nr. 105, 30 August 1978 Seite 1905 C 78 & JP-A-53 067693 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1987005530A1 (fr) * 1986-03-19 1987-09-24 Insinööritoimisto Lisop Oy Procede de purification de gaz de fumee
DE3626912A1 (de) * 1986-08-08 1988-02-11 Knauf Westdeutsche Gips Komprimate aus getrocknetem rauchgasgips und verfahren zur herstellung derselben
EP0255946A1 (fr) * 1986-08-08 1988-02-17 Gebr. Knauf Westdeutsche Gipswerke KG Produits comprimés de gypse des gaz de fumée séché et procédé de sa production
EP0266571A1 (fr) * 1986-10-08 1988-05-11 Noell-KRC Umwelttechnik GmbH Procédé de conversion des résidus des installations de désulfurisation par voie humide de gaz brulée

Also Published As

Publication number Publication date
DE3237474C2 (de) 1985-10-03
ATE18541T1 (de) 1986-03-15
DE3237474A1 (de) 1984-04-12
DE3362556D1 (en) 1986-04-17
EP0108249B1 (fr) 1986-03-12

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